Polyethylene polyamine activated organic peroxide catalyzed synthetic rubber emulsion polymerizations



Patented July 17, 1951 POLYETHY LENE POLYAMINE ACTIVATED ORGANIC PEROXIDE CATALYZED SYN- THETIC RUBBER EMULSION POLYMERI- ZATIONS Raoul L. Provost, Cheshire, Conn., assignor to United States Rubber Company, New York, N. Y., a corporation of New Jersey No Drawing. Application May 23, 1950, Serial No. 163,783

4 Claims. 1

This invention relates to improvements in polyethylene polyamine activated organic peroxide catalyzed synthetic rubber emulsion polymerizations, or so-called peroxamine polymerizations.

Increasing the reaction rate of peroxide catalyzed synthetic rubber emulsion polymerizatious by including in the polymerization recipe a reduction activator, such as a ferrous salt, is well known. Residual iron salts in the recovered rubber, however, cause decoloration of articles manufactured therefrom. There are other disadvantages, such as the necessity for carefully ageing the activating solution when reducing sugars are included with the ferrous salts. Polyethylene polyamines have been used as activators for organic peroxide catalyzed emulsion polymerizations of so-called iron-free polymerization recipes, as where iron salts are not added as such to the emulsion polymerization system, i. e. except, of course, as they might occur as impurities in other added materials. Such peroxamine polymerizations are generally carried out at temperatures below 50 F. because of the rapid reaction rate resulting from the rapid formation of free radicals by the action of the polyethylene polyamine on the organic peroxide. However, there is a tendency for reproducibility to be poor, and usually there results a very rapid rate of reaction in the first few hours of polymerization with a subsequent slowing down and sometimes total cessation of the reaction before the desired conversion of monomers into polymer has been attained. The rapid initial reaction rate is also undesirable because there then results an abnormal heat load on the cooling system through which the heat of polymerization is removed. The load is often momentarily greater than the capacity of the cooling equipment and loss of batch temperature control results which may make the polymer unsuitable for use.

By the present invention, I have been able to control the rapid initial reaction rate in peroxamine polymerizations without appreciably increasing the overall time for a given conversion of monomers to synthetic rubber, and to prevent too rapid consumption of the peroxide catalyst which leads to slowing down or cessation of reaction before the desired conversion is attained.

In carrying out the present invention, the synthetic rubber-producing polymerizable monomers are polymerized in an alkaline aqueous emulsion (pH from 9 to 12 or higher) in the presence of an organic peroxide catalyst, a polyethylene polyamine activator and, in addition, an alkali salt of ethylenediamine tetraacetic acid. The term alkali as applied to salts is used herein in its conventional meaning as including alkali-metal, ammonium and substituted ammonium (i. e. amine) salts, but excluding alkaline-earth and other polyvalent metal salts. The alkali salt of ethylenediamine tetraacetic acid in an alkaline aqueous emulsion will be the tetraalkali salt. It may be added as such to the emulsion, or it may be formed in situ in the emulsion as by adding free ethylenediamine tetraacetic acid or monoor dior tri-alkali salts of ethylenediamine tetraacetic acid to the alkaline emulsion. The amount of alkali salt of ethylenediamine tetraacetic acid in the emulsion will be from 0.001 to 0.1 part per parts of polymerizable monomers. All parts and percentages referred to herein are by weight.

The catalyst may be a conventional organic peroxide catalyst, for example, cumene hydroperoxide (alpha, alpha-di-methylbenzoyl hydroperoxide), tertiary butyl hydroperoxide, diisopropylbenzene hydroperoxide, cyclohexylbenzene hydroperoxide, cymene hydroperoxide, etc. The amount of organic peroxide catalyst will generally be from 0.05 to 0.5 part per 100 parts of polymerizable monomers. The polyethylene polyamine activators for the organic peroxide catalyst are well known materials and may be one or a mixture of polyethylene polyamines. Effective activators are diethylene triamine, triethyl- ,ene tetraamine, tetraethylene pentamine, and

the higher polyethylene polyamines up to mixtures of high molecular weight polyethylene polyamines having an average molecular weight of over a thousand, as in the still bottom from the distillation recovery of the lower polyethylene polyamines (and ethylene diamine) from the autoclave reaction product of ethylene dichloride and ammonia, which has a molecular weight around 1200. The amount of polyethylene polyamine will generally be from 0.01 to 0.5 part per 100 parts of polymerizable monomers. Conventional polymerization regulators such as aliphatic mercaptans having 6 to 18 carbon atoms (Cs to C12), and aromatic mercaptans may be used to regulate the polymer chain length. The emulsifying agents for the polymerizable monomers may be the conventional water-soluble soaps of soap-forming monocarboxylic acids, such as the alkali salts of aliphatic acids having 8 to 24 carbon atoms, rosin acids, or naphthenic acids, or other anionic surface-active emulsifying and dispersing agents. The polyethylene polyamines activate the organic peroxide catalysts in alkaline medium. Alkali soaps and hydroxides will render the aqueous emulsion alkaline as in conventional polymerizations. The polymerization is allowed to take place at the desired temperature until the desired conversion of monomers to synthetic rubber, generally 50% to 85% conversion, is reached. Iron-free peroxyamine polymerization recipes are primarily used in commercial socalled cold GR-S polymerizations at 41 F., and the present invention is particularly adapted to such cold GR- S polymerizations, but may be used with GR-S and other synthetic rubber polymerizations at various temperatures, as from 32 F. to 150 F. After conversion of the desired amount of pohrmerizable monomers to synthetic rubber, the polymerization is stopped by the addition of a so-called shortstopping agent which prohibits further polymerization of the monomers during their removal. Hydroquinone, di-tert-butyl hydroquinone, and dinitrochlorobenzene are common shortstopping agents. After addition of the shortstopping agent, the unreacted residual polymerizable monomers are removed from a synthetic rubber latex. as by venting ofi monomers, e. g. butadiene-1,3, which are gaseous at atmospheric pressure, and by steam distilling under reduced pressure the residual higher boiling point or liquid monomers, e. g., styrene, and the thus recovered polymerizable monomers may be utilized in subsequent emulsion polymerizations. If desired, the synthetic rubber latex may be ccagulated by salt and/or acid in known manner.

The polymerizable material in the preparation of the synthetic rubber latex may be one or a mixture of butadienes-L3, for example, butadione-1,3, methyl-2-butadiene-l,3 (isoprene) chloro-2-butadiene-l,3 (chloroprene) piperylene, 2,3- dimethyl butadiene-l,3. The polymerizable material, as is known, may be a mixture of one or more such butadienes with one or more polymerizable compounds which are capable of forming rubber copolymers with butadienes-l,3; for example, up to -70% of such mixture of one or more compounds which contain a single CH2=C group where at least one of the disconnected valences is attached to an electro-negative group, that is, a group which substantially increases the electrical dissymmetry or polar character of the molecule. Examples of such monooleflnes containing a terminal methylene (CH2=C group which are copolymerizable with butadienes-1,3, are aryl olefines, such as styrene, vinyl naphthylene; alpha methyl styrene, parachloro styrene, dichloro styrene; the alpha methylene carboxylic acids and their esters, nitriles and amides, such as acrylic acid, methyl acrylate, methyl methacrylate, acrylonitrile, methacrylonitrile, methacrylamine; methyl vinyl ether, methyl vinyl ketone; vinylidene chloride.

The following examples are illustrative of the present invention:

Example I Two reactors were charged with a conventional GR-S peroxamine polymerization formulation as follows: 71 parts of butadiene-l,3, 29 parts of styrene, 4.7 parts of the sodium soap of disproportionated rosin acid (emulsifier), 0.2 part of sodium hydroxide, 0.05 part of the condensation product of formaldehyde and sodium naphthalene sulfonate (additional anionic emulsifying and dispersing agent), 0.12 part of tertiary dpdecyl mercaptan (polymerization modifier or regulator), 0.15 part of diisopropylbenzene hydroperoxide (catalyst), 0.08 part of tetraethylene pentamine, and 200 parts of water (including water added to the reactor as such and'the water used to make up the various emulsions and solutions of the added reagents). To the charge in one of the reactors only, there was added 0.008 part of ethylenediamine tetraacetic acid.

The emulsions of polymerizable monomers were polymerized at 41 F. under agitation until 60 percent conversion of polymerizable monomers to synthetic rubber. The 60% conversion 0! the emulsion to which the ethylenediamine tetraacetic acid was added took 18 hours while the other (control) emulsion took 17 hours. However, the conversion of monomers to polymer in the control batch was exceedingly rapid in the early stages of the polymerization with consequent evolution of correspondingly large amounts of heat, whereas the conversion of monomers to polymer in the batch to which the ethylenediamine tetraacetic acid had been added was slower in the early stages of the polymerization, but with substantially the same overall time for the desired conversionsof 60% of the original polymerizable monomers to polymer. The rates of 1 conversion of the two batches is shown in the following table, batch A being the control and batch B containing the ethylenediamine tetraacetic acid:

Conversion Time Hours Per cent Per cent 3 23 10 6 37 21 9 45 28 i2 54 42 15 58 54 As shown in the above table, the addition of a small amount of ethylenediamine tetraacetic acid effectively controlled and evened out the rate of polymerization.

Example it Two reactors were charged with another GR-S peroxamine polymerization recipe containing no iron salts added as such. The formulation contained 71 parts of butadiene-l,3, 29 parts of styrene, 4.72 parts of oleic acid, 5.82 parts of ammonium hydroxide (to neutralize the oleic acid and form soap emulsifier), 0.39 part of acetic acid (to form ammonium acetate with ammonium hydroxide to reduce the viscosity), 0.15 part of tertiary dodecyl mercaptan, 0.15 part of diisopropylbenzene hydroperoxide, 0.08 part of tetraethylene pentamine, and 200 parts of water. To the charge in one of the reactors. only, there was added 0.008 part' of ethylenediamine tetraacetic acid.

The emulsions were polymerized at 41 F. under agitation until 60 per cent conversion of polymerizable monomers to synthetic rubber.

The conversion in three hours in the case of the control was 25 percent whereas the conversion in the batch containing the ethylenediamine tetraacetic acid was 14 percent. However, it took the control batch 30 hours for 60% conversion whereas it took the batch containing the ethylenediamine tetraacetic acid only 14 ,hours for 60 percent conversion. The rapid conthe principles underlying the invention, reference should be made to the appended claims for an understanding of the scope of theprotection aiforded the invention.

Having thus described my invention what I claim and desire to protect by Letters Patent is:

1. In the process of emulsion polymerizing in alkaline medium and iron-free synthetic rubber polymerization recipe comprising synthetic rubher-forming monomers selected from the group consisting of butadienes-1,3 and mixtures of butadienes-l,3 with compounds which contain a single CH2=C group and are copolymerizable with butadienes-1,3, water, emulsifying agent. organic peroxide catalyst and polyethylene polyamine activator, the step which comprises carrying out the polymerization in the presence of 0.001 to 0.1 part of alkali salt of ethylenediamine tetraacetic acid per 100 parts of polymerizable monomers.

2. The process which comprises polymerizing an alkaline aqueous emulsion of polymerizable synthetic rubber-forming monomers selected from the group consisting of butadienes-l,3 and mixtures of butadienes-L3 with compounds which contain a single CH2=C group and are copolymerizable with butadienes-1,3, and containing emulsifying agent, organic peroxide catalyst and polyethylene polyamine activator, said emulsion containing iron salts only as impurities and containing 0.001 to 0.1 part of alkali salt of ethylenediamine tetraacetic acid per 100 parts of polymerizable monomers.

3. In the process of emulsion polymerizing in alkaline medium an iron-free synthetic rubber polymerization recipe comprising a mixture of butadiene-1,3 and styrene, water, emulsifying agent, organic peroxide catalyst and polyethylpolymerizablemonomers.

RAOUL L. PROVOST.

REFERENCES CITED The following references are of record in the -flle of this patent:

Mitchell et al., Ind. and Eng. Chem, Aug. 1949, pp. 1592-1599.

Whitby et al., Abstract in Rubber Age, vol. 65, No. 5, Aug. 1949, page 545. 

1. IN THE PROCESS OF EMULSION POLYMERIZING IN ALKALINE MEDIUM AND IRON-FREE SYNTHETIC RUBBER POLYMERIZATION RECIPE COMPRISING SYNTHETIC RUBBER-FORMING MONOMERS SELECTED FROM THE GROUP CONSISTING OF BUTADIENES-1,3 AND MIXTURES OF BUTADIENES-1,3 WITH COMPOUNDS WHICH CONTAIN A SINGLE CH2=C< GROUP AND ARE COPOLYMERIZABLE WITH BUTADIENES-1,3, WATER, EMULSIFYING AGENT, ORGANIC PEROXIDE CATALYST AND POLYETHYLENE POLYAMINE ACTIVATOR, THE STEP WHICH COMPRISES CARRYING OUT THE POLYMERIZATION IN THE PRESENCE OF 0.001 TO 0.1 PART OF ALKALI SALT OF ETHYLENEDIAMINE TETRAACETIC ACID PER 100 PARTS OF POLYMERIZABLE MONOMERS. 